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Publication numberUS5716591 A
Publication typeGrant
Application numberUS 08/351,541
Publication dateFeb 10, 1998
Filing dateDec 7, 1994
Priority dateJan 27, 1992
Fee statusLapsed
Also published asDE69305661D1, DE69305661T2, EP0553921A1, EP0553921B1
Publication number08351541, 351541, US 5716591 A, US 5716591A, US-A-5716591, US5716591 A, US5716591A
InventorsAntonio Crispoldi
Original AssigneeNuova Terni Industrie Chimiche S.P.A.
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Process for producing calcium nitrate-urea adduct
US 5716591 A
Abstract
Calcium nitrate-urea adduct, a product having the formula Ca(NO3)2.4CO(NH2)2 !, is obtained by means of a process which basically consists of the following steps:
mixing molten urea and calcium nitrate;
feeding the resulting solution to a turbodryer;
feeding the resulting molten salt to a granulator drum;
recovery of calcium nitrate-urea adduct.
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Claims(1)
I claim:
1. A process for producing solid, granular, free-flowing calcium nitrate-urea, which process comprises the following steps:
(a) preparing, at a temperature not higher than 170 C., a solution comprising urea and calcium nitrate and having a water content of up to 18% by weight, wherein the molar ratio of urea to calcium nitrate is about 4/1;
(b) feeding the solution prepared in step (a) to a turbodryer via an inlet having a temperature of from 120 C. to 170 C. so as to produce an essentially anhydrous molten salt from the solution, said turbodryer consisting essentially of (i) a cylindrical shell heated from the outside with diathermic oil circulated in a closed loop, and (ii) a rotatably affixed shaft with paddles rotating at a speed of about 400 revolutions per minute;
(c) feeding the molten salt produced in step (b) to a granulation zone so as to produce solid, granular, free-flowing calcium nitrate-urea, said zone comprising a rotary cylindrical drum (i) revolving around its axis, (ii) having longitudinal baffles integral with the inner surface thereof, (iii) a fluidized bed situated along its axis, which bed is fed, from its interior, with room air having a temperature of from 60 C. to 120 C., and (iv) a beam bearing spraying nozzles situated under the fluidized bed; and
(d) recovering solid, granular, free-flowing calcium nitrate-urea produced in step (c).
Description

This application is a continuation of U.S. Ser. No. 08/009,123, filed Jan. 26, 1993, now abandoned.

FIELD OF THE INVENTION

The present invention relates to an improved process for producing calcium nitrate-urea adduct as a granular, free-flowing solid material which has been used in the past, as such, in agriculture, as a nitrogenous fertilizer. In a narrower sense, the invention also relates to some equipment pieces useable in order to carry out such a process.

BACKGROUND OF THE INVENTION

Calcium nitrate-urea adduct is a per se known compound and is an addition product of calcium nitrate and urea, in which calcium nitrate constitutes 40.6% by weight, and can be defined by means of the formula Ca(NO3)2.4CO(NH2)2 !.

Calcium nitrate-urea adduct potentially is a very interesting compound as a fertilizer, because, additionally to ureic nitrogen, it contains nitric nitrogen, the presence of which makes it possible the typical ammonia losses shown by urea alone, when the latter undergoes the hydrolysis process in the soil, to be avoided.

In spite of the above, calcium nitrate-urea adduct did not find heretofore a meaningful commercial success, above all owing to the difficulties met when one wishes to obtain that product with suitable physical characteristics for its use as an agricultural fertilizer.

For example, processing calcium nitrate-urea adduct through crystallization, prilling and rotary-tray granulation does not make it possible a granular, free-flowing product with no tendency to release dusts, to be obtained.

In the art also a fluidized bed processing was proposed, a technique which meets with operating difficulties and requires the use of complex equipment pieces.

Furthermore, the product which can be obtained in that way contains an excess of urea over to the required urea amount in order to form the adduct, and also characterized by the undesirable characteristic of low values of granules hardness,

From Italian patent application No. 19 363A/87 filed on Feb. 13th, 1987, a process is known which makes it possible the above reminded drawbacks to be partially overcome, according to which process:

a liquid composition is prepared, at a temperature of not more than 170 C., which contains urea and calcium nitrate;

said liquid composition is sprayed onto previously formed, solid particles of calcium nitrate-urea adduct, kept in movement;

calcium nitrate-urea adduct is recovered from said solid spraying products,

The resulting calcium nitrate-urea adduct is in the form of a granular solid material and can be used in agriculture as a nitrogen containing fertilizer,

Unfortunately, directly feeding the liquid composition obtained from the first step, under the action of a hot gas, onto previously formed solid particles of calcium nitrate-urea adduct, for example kept moving inside a rotary drum, does not eliminate all of the drawbacks briefly mentioned hereinabove; in particular, not always granules can be obtained which are all free-flowing, or endowed with perfectly homogeneous mechanical characteristics.

SUMMARY OF THE INVENTION

Therefore, the subject-matter of the present invention is an improved process for producing calcium nitrate-urea adduct, which makes it possible a perfectly granular and free-flowing product to be obtained which is absolutely homogeneous as regards the mechanical characteristics of the various particles, which process substantially comprises the following steps:

(a) mixing molten urea and calcium nitrate;

(b) feeding the resulting solution to a turbodryer;

(c) feeding the resulting molten salt to a granulation zone;

(d) recovery of calcium nitrate-urea adduct.

In particular, in the (a) step a liquid composition is prepared at a temperature not higher than 170 C., which contains urea and calcium nitrate in a mutual molar ratio equal, or approximately equal, to 4:1, and containing a water content of up to 18% by weight.

In order to prepare such a liquid composition, calcium nitrate can be used as a dried powder, or as a concentrated aqueous suspension containing a water content of up to values of the order of 15-18% by weight.

Furthermore, the calcium nitrate used may contain ammonium nitrate as an impurity, up to levels of the order of 5-6% by weight.

Urea used in the preparation of such a composition normally shows a purity of the order of 97% by weight or more, and may contain biuret as an impurity, in an amount of up to approximately 1.2% by weight.

The preparation of such a liquid composition can be carried out according the normal techniques well known to those skilled in the art, or according to as disclosed in the disclosure of the Italian patent application No. 19 363A/87 mentioned above, to which reference is made of course for any further details.

The solution obtained in that way contains water which, if sent to the granulation step, could cause those unevenness drawbacks already mentioned above.

According to the process of the present invention, the solution obtained from the preliminary mixing step (a) step! is sent, at a temperature comprised within the range of from 120 to 170 C., to a particular turbodryer (b) step!, with, in that way, anhydrous, molten calcium nitrate-urea adduct at the temperature of 150-200 C. being directly obtained at the outlet.

According to a preferred embodiment of the present invention, the turbodryer is basically constituted by a cylindrical shell heated from the outside with closed-loop circulated diathermic oil.

Said oil is kept at its operating temperature by heating by means of a heating unit.

Inside said cylindrical shell and coaxial with it, shaft is provided which is equipped with a plurality of paddles and is kept revolving at a revolution speed preferably of round 400 g/minute. Said paddles perform the task of distributing the entering solution along the walls of the cylindrical chamber, so as to realize a thin-film concentration.

Said equipment may operate either in the presence or in the absence of a flowing stream of hot air.

The resulting molten salt is sent, through a suitable pump, to a fluidized-bed granulator drum.

Still according to a a preferred embodiment, the granulator can be constituted by a cylindrical drum revolving around its own axis at a revolution speed which is comprised within the range of from 8 to 12 revolution per minute, which cylindrical drum is equipped with longitudinal baffles integral with the internal surface of the same cylindrical drum.

Along the axis of the drum, the fluidized bed is positioned, and under it there is the beam which supports the spraying nozzles. The baffles perform the task of moving the calcium nitrate-urea adduct granules towards the high side of the drum, so that they may then be caused to fall back into the cooling fluidized bed; during the subsequent falling of the salt from the fluidized bed towards the bottom of the drum, a curtain is formed onto which calcium nitrate-urea adduct sprayed by the nozzles impinges.

The fluidized bed is fed, from its interior, with room air heated at a temperature comprised within the range of from 60 to 120 C.: it performs the purpose of removing the melting heat of the granules which are being formed.

The temperature at the outlet from the granulator is comprised within the range of from 80 to 115 C.

The product is then sent to the sieving and recycle system. Also a step of post-drying of the so separated granules can be added, in order to reach optimal hardness values. Also the use of a hardening agent can be provided for.

For these operations too, as well as for alternative solutions to the rotary drum as disclosed above, those skilled in the art may select any from the large number of operating ways which are suggested from the prior art or, also, stick to indications supplied by the above mentioned Italian patent application No. 363A/87, the disclosure of which, for the pertinent portions, is incorporated herein by reference.

BRIEF DESCRIPTION OF THE DRAWINGS

The accompanying FIGURE illustrates a flow chart of a preferred embodiment of the invention.

DETAILED DESCRIPTION OF A PREFERRED EMBODIMENT OF THE INVENTION

The following illustrative, non-limitative, example, contributes to a better understanding of the present invention, of which it supplies further details.

EXAMPLE

Referring to the flow chart shown in the FIGURE, in order to obtain 1000 kg of calcium nitrate-urea adduct:

(A) From line (1) to the vessel (3) molten calcium nitrate with the following characteristics:

Temperature=135 C.

kg=500

Composition: Ca(NO3)2 =79% by weight

NH4 NO3 =6% by weight

H2 O=15% by weight is fed to the vessel (3).

From line (2), molten urea having the characteristics:

Temperature=136 C.

kg=574.7

Composition: CO(NH2)2 =98.8% by weight

biuret=0.8% by weight

H2 O=0.4% by weight enters said reaction vessel (3).

(B) Inside the reaction vessel (3) the reaction takes place with heat being developed which is removed from the system by means of a water cooled coil (4).

At the outlet (5) from the reaction vessel, a solution of calcium nitrate-urea adduct is obtained with the following characteristics:

Temperature=115-125 C.

kg=about 1075

Composition: CO(NH2)2 =52.8% by weight

Ca(NO3)2 =36.7% by weight

NH4 NO3 =2.8% by weight

biuret=0.4% by weight

H2 O=7.2% by weight

(C) The resulting calcium nitrate-urea adduct solution is fed to a thin-film turbodryer (6) where the evaporation of water takes place and at the outlet (7) molten calcium nitrate-urea adduct is obtained a temperature of approximately 180 C., which by analysis is shown to have the following composition:

CO(NH2)2 =56.3% by weight

Ca(NO3)2 =39.4% by weight

NH4 NO3 =3.0% by weight

biuret=0.8% by weight

H2 O=0.5% by weight

The jacket of the turbodryer is kept hot by circulating (8) diathermic oil at the temperature of about 250 C., and inside the interior of the turbodryer a stream of hot air (9) is flown, which facilitates stripping steam from the mass which is being concentrated.

(D) The molten product, which is at the temperature of 180 C., is sent (12) to the granulator (11) by means of the release pump (10), then is cooled (14) with room air, so that the leaving granulate (13) is at a temperature comprised within the range of from 80 to 115 C. Air is then sent to the scrubber (15).

(E) The granulate is sieved, then is cooled in the fluidized bed (16), and is subsequently sent to the packaging step (17).

The fluidized bed feeding air (18) is cold and dried: temperature 10 C., and saturated at 4 C. Characteristics of the end product:

Amount=1000 kg

CO(NH2)2 =56.2% by weight

Ca(NO3)2 =39.4% by weight

NH4 NO3 =3.3% by weight

Biuret=0.9% by weight

H2 O=0.2% by weight

Total N=34.5% by weight

Nitric N=7% by weight

Granulometry=95% comprised within the range of from 2 to 4 mm

Hardness of granules=4000 g

Patent Citations
Cited PatentFiling datePublication dateApplicantTitle
US3475132 *Dec 23, 1964Oct 28, 1969Inventa AgFluidized bed for the granulation of fertilizers
US4091544 *Feb 11, 1977May 30, 1978The Procter & Gamble CompanyDrying process
US4497757 *Jan 31, 1983Feb 5, 1985The Procter & Gamble CompanyForming spheres from a water wet mixture of sodieum sulfate and non-hydratable materials
US4749349 *Dec 5, 1985Jun 7, 1988Kaltenbach-Thuring S.A.Granulating device and plant
US4874595 *Feb 5, 1988Oct 17, 1989Enichem Agricoltura S.P.A.Process for producing calcium-urea nitrate
CS663273A * Title not available
EP0278562A2 *Feb 3, 1988Aug 17, 1988ENICHEM AGRICOLTURA S.p.A.Process for producing calcium urea-nitrate
Non-Patent Citations
Reference
1 *Derewent Abstract No. 663273, Nov. 1987.
Classifications
U.S. Classification423/397, 504/158, 564/32, 504/327, 564/63, 504/163
International ClassificationC05C13/00, C05C5/00, C05C5/04, F26B17/24, C05C9/00
Cooperative ClassificationC05C5/04, C05C5/005, C05C9/00, F26B17/24
European ClassificationC05C5/04, C05C5/00B, C05C9/00, F26B17/24
Legal Events
DateCodeEventDescription
Apr 9, 2002FPExpired due to failure to pay maintenance fee
Effective date: 20020210
Feb 11, 2002LAPSLapse for failure to pay maintenance fees
Sep 4, 2001REMIMaintenance fee reminder mailed
Jul 1, 1997ASAssignment
Owner name: NUOVA TERNI INDUSTRIE CHIMICHE S.P.A., ITALY
Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:TERNI INDUSTRIE CHIMICHE S.P.A.;REEL/FRAME:008622/0961
Effective date: 19970613